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鎳電解陽極液深度凈化除鉛

Deep lead removal from anodic electrolyte of nickel electrolysis

  • 摘要: 為了處理含高鉛的鎳物料,進行了電解陽極液中深度除鉛的實驗研究.分析了電解鎳含鉛量與電解液中Pb2+質量濃度的關系、共沉淀凈化除鉛的機理及電解液中的Cl-、Fe3+對除鉛結果的影響.通過實驗研究,確定了采用共沉淀法深度除鉛的最優技術參數:氯化鋇加入系數為150、除鉛溫度為55℃、攪拌除鉛時間為60 min、噴淋加入氯化鋇溶液的時間為21 min、絮凝劑的質量濃度為2.5 g·L-1.實驗結果表明:采用氯化鋇共沉淀法凈化除鉛,除鉛后電解液中Pb2+≤0.0003 g·L-1,渣含鎳質量分數小于4%,滿足電解鎳生產對電解液成分的要求.通過除鉛擴大試驗,證明了小型試驗所確定的技術參數的可靠性,該工藝成功地應用于工業生產實踐.

     

    Abstract: In order to deal with nickel materials which contain high lead,experimental investigations were performed to remove deeply lead from anodic electrolyte.By analyzing the relationship of Pb2+ concentration in electrolyte and lead content in electrolytic nickel,the mechanism of lead removal by coprecipitation,and the effects of Cl- and Fe3+ on the results of lead removal,some optimum technological parameters were determined for deep lead removal by coprecipitation: the coefficient of adding barium chloride is 150,the temperature of lead removal is 55 ℃,the time of lead removal by stirring and the time of adding barium chloride solution by spraying are 60 min and 21 min respectively,and the mass concentration of flocculant is kept constant at 2.5 g·L-1. It is shown that lead can be removed by coprecipitation with barium chloride,the mass concentration of Pb2+ is not more than 0.000 3 g·L-1 in lead removal electrolyte,and the mass fraction of nickel in slag is less than 4%,which meet the need of producing electrolytic nickel for electrolyte composition.The enlarged experiments prove that the technological parameters derived from the laboratory experimenters are reliable and the process has been applied to industrial production successfully.

     

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